P
US10150828B2ActiveUtilityPatentIndex 70

Process for producing propylene terpolymers

Assignee: CAVALIERI CLAUDIOPriority: Aug 3, 2007Filed: Jul 29, 2008Granted: Dec 11, 2018
Est. expiryAug 3, 2027(~1.1 yrs left)· nominal 20-yr term from priority
Inventors:CAVALIERI CLAUDIOCAGNANI CAMILLOGUIDICINI ALESSANDRO
C08F 210/16C08F 2/34C08F 210/06C08J 5/18C08J 2323/14C08F 2/001C08F 2500/12C08F 4/6494C08F 210/08C08F 2500/21C08F 2500/26C08F 4/651C08F 4/647
70
PatentIndex Score
3
Cited by
16
References
9
Claims

Abstract

The present invention further relates to the propylene terpolymer obtained by said process particularly suitable to be used as films such as cast films, bi- or mono-oriented films and heat-sealable films having good optical properties and excellent sealing properties combined with good shrinkage properties and softness.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
       1. A process for producing a propylene terpolymer in a single gas-phase polymerization reactor comprising two interconnected polymerization zones comprising the steps of:
 (a) feeding a first gas mixture comprising: 
 (i) a first concentration of propylene; 
 (ii) a first concentration of ethylene; and 
 (iii) a first concentration of a butene;
 into a first interconnected polymerization zone in the presence of a catalyst for producing a polymer; 
 
 (b) directing the polymer into a second interconnected polymerization zone; 
 (c) re-introducing the polymer into the first interconnected polymerization zone; and 
 (d) recovering the propylene terpolymer comprising:
 (i) ethylene derived units; 
 (ii) propylene derived units; and, 
 (iii) butene derived units; 
 wherein the total content of ethylene and butene derived units are present in the propylene terpolymer in an amount not less than 8% by weight, based on the total weight of the propylene terpolymer, 
 wherein the weight ratio of ethylene to butene ranges from 0.21:1 to 0.52:1, 
 wherein when the ethylene content ranges from 2.30 to 3.10% by weight, based on the total weight of the propylene terpolymer, the butene content is higher than 5.9% by weight, based on the total weight of the propylene terpolymer, and 
 wherein the propylene terpolymer comprises 10-13.9 wt. % of a xylene soluble fraction based upon the total weight of the propylene terpolymer and a flexural modulus of less than 750 MPa. 
 
 
     
     
       2. The process of  claim 1 , wherein the first concentration of butene ranges from 7 to 20 mole % based upon the total molar amount of propylene, ethylene and butene present in the first gas mixture. 
     
     
       3. The process of  claim 1 , wherein the catalyst is a Ziegler-Natta catalyst comprising a solid catalyst component wherein the solid catalyst component comprises:
 (i) magnesium chloride; 
 (ii) at least one titanium compound having at least one titanium-halogen bond; and 
 (iii) at least one electron-donor compound; 
 wherein the at least one titanium compound and the at least one electron-donor compound are supported on magnesium chloride. 
 
     
     
       4. The process of  claim 1 , wherein the first concentration of ethylene ranges from 0.5 to 5 mole % based upon the total molar amount of propylene, ethylene and butene present in the first gas mixture. 
     
     
       5. The process of  claim 1 , wherein the propylene terpolymer has a sealing initiation temperature ranging from 100 to 116° C., a fraction soluble in hexane lower than 6 wt % and a melt flow index ranging from 0.1 to 100 g/10 min. 
     
     
       6. A propylene terpolymer film comprising the propylene terpolymer produced in accordance with  claim 1 , wherein said film is characterized by a haze percentage of less than 0.7% and a gloss percentage of greater than 88.5%. 
     
     
       7. The propylene terpolymer film of  claim 6 , wherein said film is characterized by a shrinkage percentage of greater than 30% at a temperature of 110° C. 
     
     
       8. The propylene terpolymer film of  claim 6 , wherein said film is characterized by a flexural modulus value in a range of 500 to 700 MPa. 
     
     
       9. The process of  claim 1 , wherein the first interconnected polymerization zone is a riser and the second interconnected polymerization zone is a downcomer.

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